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CN111939896B - Liquid catalyst for catalyzing ozone decomposition at normal temperature and its preparation method and application - Google Patents

Liquid catalyst for catalyzing ozone decomposition at normal temperature and its preparation method and application Download PDF

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CN111939896B
CN111939896B CN202010750335.0A CN202010750335A CN111939896B CN 111939896 B CN111939896 B CN 111939896B CN 202010750335 A CN202010750335 A CN 202010750335A CN 111939896 B CN111939896 B CN 111939896B
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room temperature
ozone
liquid catalyst
ozonolysis
salt
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CN111939896A (en
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卢晗锋
陈晓
周瑛
胡中恒
耿俊
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Zhejiang University of Technology ZJUT
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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    • B01J23/34Manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8671Removing components of defined structure not provided for in B01D53/8603 - B01D53/8668
    • B01D53/8675Ozone
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/002Mixed oxides other than spinels, e.g. perovskite
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    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/889Manganese, technetium or rhenium
    • B01J23/8892Manganese
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    • B01J35/20Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
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    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
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Abstract

A liquid catalyst for catalyzing ozonolysis at normal temperature is prepared by the following method: dissolving metal salt in water, adding a complexing agent and a surfactant, and uniformly stirring to obtain a mixed solution; stirring the obtained mixed solution at room temperature to 95 ℃ for 0-40 min, then adding a solvent, crystallizing at 120-200 ℃ for 1-8 h, cooling to room temperature, performing suction filtration, filtering out solids, and dispersing the solids in the solvent to obtain the product; the active spraying liquid prepared by the invention does not need to be roasted, can be used for flexibly atomizing and spraying loads on the surfaces of objects with any shapes and materials theoretically, and can endow the objects with the capability of catalyzing and decomposing ozone after being dried, so that the space is fully utilized, the ozone is fully contacted with a catalytic material as far as possible, the environmental ozone is further decomposed efficiently, and the purpose of treating ozone pollution is achieved.

Description

常温催化臭氧分解的液体催化剂及其制备方法与应用Liquid catalyst for catalyzing ozone decomposition at room temperature, preparation method and application thereof

技术领域technical field

本发明涉及一种常温催化臭氧分解的液体催化剂及其制备方法和应用。The invention relates to a liquid catalyst for catalyzing ozone decomposition at room temperature, a preparation method and application thereof.

背景技术Background technique

空气是人类赖以生存、一刻也不能缺少的必需物质,其质量直接影响着人类的生产和生活。近年来,我国臭氧超标问题日益突出,成为继PM2.5之后又一个重要的区域性大气污染物。臭氧作为一种强氧化性气体,对人的皮肤和眼睛具有腐蚀作用,能强烈刺激机体黏膜组织,当浓度超过1×10-7(体积比)时会引起人体不适,导致气喘、支气管炎、心脏病等心肺问题,浓度进一步提高甚至会导致死亡。另外,臭氧还会对生态环境造成损害,比如,引起植物叶片坏死、脱落,造成农作物减产等。因此,必须对臭氧污染进行有效治理,这就需要一种高效安全的臭氧去除方法。Air is an essential substance that human beings cannot live without for a moment, and its quality directly affects human production and life. In recent years, the problem of excessive ozone in my country has become increasingly prominent, and it has become another important regional air pollutant after PM2.5. As a strong oxidizing gas, ozone has a corrosive effect on human skin and eyes, and can strongly stimulate the mucous membrane tissue of the body. When the concentration exceeds 1×10 -7 (volume ratio), it will cause discomfort to the human body, resulting in asthma, bronchitis, Cardiopulmonary problems such as heart disease, further increase in concentration can even lead to death. In addition, ozone can also cause damage to the ecological environment, for example, causing necrosis and shedding of plant leaves, resulting in reduced crop production. Therefore, it is necessary to effectively control ozone pollution, which requires an efficient and safe ozone removal method.

目前臭氧去除方法主要有热分解法、活性炭法、药液吸收法和催化分解法等。其中,催化分解法因具有安全、经济和高效等特点是目前普遍认可和关注的臭氧污染治理方法。催化分解法的核心是催化剂,关键在于高性能催化剂的研发。如:CN110433795A公开了一种活性炭负载MnOx催化剂、其制备方法及其应用,以二价锰盐、碳酸氢铵、活性炭和十二烷基硫酸钠为原料,通过共沉淀法制备得到催化剂前驱体,再利用高温热处理的方法,制备出MnOx均匀负载在活性炭上且粒径可控的活性炭负载MnOx催化剂,将该催化剂应用于催化分解臭氧材料中,能在室温下有效催化分解臭氧。CN110420636A公开了一种镧改性的锰氧化物催化剂、其制备方法及其应用,通过将二价锰盐与高锰酸盐或过硫酸盐进行水热处理制得锰氧化物,再在锰氧化物中掺杂镧盐,经干燥与高温灼烧处理后即可得到镧改性的锰氧化物催化剂,制得的镧改性的锰氧化物催化剂能在室温下高效地催化分解臭氧,相较未经过镧改性的锰氧化物,其大大缩短了室温下分解臭氧所需的时间。CN105312061提供了一种常温除臭氧催化材料,以高比表面积的多孔活性炭、分子筛为主的复合材料为载体;负载有一种或几种非贵金属氧化物为活性组分,同时载有一种或几种还原性保护剂,采用分步浸渍工艺,再通过焙烧制备而成,在常温常湿条件下催化分解臭氧能力可达95%以上。At present, the ozone removal methods mainly include thermal decomposition method, activated carbon method, chemical liquid absorption method and catalytic decomposition method. Among them, the catalytic decomposition method is the ozone pollution control method that is generally recognized and concerned because of its safety, economy and high efficiency. The core of the catalytic decomposition method is the catalyst, and the key lies in the research and development of high-performance catalysts. Such as: CN110433795A discloses a kind of activated carbon supported MnO x catalyst, its preparation method and its application, with divalent manganese salt, ammonium bicarbonate, activated carbon and sodium lauryl sulfate as raw materials, the catalyst precursor is prepared by co-precipitation method , and then using the method of high temperature heat treatment, an activated carbon-loaded MnO x catalyst with MnO x uniformly loaded on activated carbon and with controllable particle size was prepared. This catalyst was applied to catalytic decomposition of ozone materials, which can effectively catalyze the decomposition of ozone at room temperature. CN110420636A discloses a lanthanum-modified manganese oxide catalyst, its preparation method and its application. Manganese oxide is obtained by hydrothermally treating divalent manganese salt with permanganate or persulfate, and then the manganese oxide is Doped with lanthanum salt, after drying and high-temperature calcination, the lanthanum-modified manganese oxide catalyst can be obtained. The prepared lanthanum-modified manganese oxide catalyst can efficiently catalyze and decompose ozone at room temperature. Manganese oxide modified with lanthanum, which greatly shortens the time required to decompose ozone at room temperature. CN105312061 provides a catalytic material for removing ozone at room temperature, which uses porous activated carbon with a high specific surface area and a composite material based on molecular sieve as a carrier; one or more non-precious metal oxides are loaded as active components, and one or more The reductive protective agent is prepared by step-by-step impregnation process and then roasted. It can catalyze and decompose ozone by more than 95% under normal temperature and humidity conditions.

如上所述,研究人员已报道了许多性能优异的非贵金属氧化物臭氧常温分解催化剂。但是,环境臭氧与一般工业有组织排放的废气有显著区别,其不仅浓度极低且在空间高度分散,所以目前所报道的常规结构催化剂用于治理环境臭氧时无法有效发挥作用。要实现臭氧污染高效分解必须解决以下两个问题:(1)如何提高臭氧与催化剂的接触面?(2)如何提高极低浓度臭氧在催化剂表面的分解速率?因此,亟需开发性能更为优异且能与高分散臭氧充分接触的新型臭氧常温分解催化剂。As mentioned above, researchers have reported many non-noble metal oxide ozonolysis catalysts with excellent performance. However, ambient ozone is significantly different from the exhaust gas emitted by general industrial organizations. It is not only extremely low in concentration but also highly dispersed in space. Therefore, the conventional structure catalysts reported so far cannot effectively play a role in the treatment of ambient ozone. In order to achieve efficient decomposition of ozone pollution, the following two problems must be solved: (1) How to improve the contact surface between ozone and catalyst? (2) How to improve the decomposition rate of extremely low concentration ozone on the catalyst surface? Therefore, there is an urgent need to develop a new type of ozone decomposition catalyst with better performance and full contact with highly dispersed ozone.

发明内容Contents of the invention

针对目前常规结构催化剂催化分解环境臭氧时存在的不足,我们的解决思路是设计合成稳定的高活性、高比表面金属氧化物液体催化剂,通过雾化喷洒负载方法,在任意结构的支撑体表面形成均匀分散且牢固的高活性催化剂膜,从而不受支撑体形式限制,把任意形状结构的支撑体变为催化剂,充分利用反应空间,有效提高环境臭氧与催化剂的接触面,提高催化效率,这是一种全新的环境臭氧治理方案。Aiming at the deficiencies existing in the catalytic decomposition of ambient ozone by catalysts with conventional structures at present, our solution is to design and synthesize a stable high-activity, high-specific-surface metal oxide liquid catalyst, which can be formed on the surface of a support with any structure by atomizing and spraying the loading method. Uniformly dispersed and firm high-activity catalyst film, so that it is not limited by the form of the support, and the support of any shape and structure can be turned into a catalyst, making full use of the reaction space, effectively improving the contact surface between ambient ozone and the catalyst, and improving the catalytic efficiency. A brand-new environmental ozone control scheme.

本发明的技术方案如下:Technical scheme of the present invention is as follows:

一种常温催化臭氧分解的液体催化剂,按如下方法制备得到:A liquid catalyst that catalyzes the decomposition of ozone at room temperature is prepared as follows:

将金属盐溶于水,加入络合剂和表面活性剂搅拌均匀,得到混合溶液;将所得混合溶液于室温~95℃下搅拌0~40min,之后加入溶剂,在120~200℃下晶化1~8h,冷却至室温,抽滤,滤出固体分散在溶剂中,即得所述常温催化臭氧分解的液体催化剂;Dissolve the metal salt in water, add a complexing agent and a surfactant and stir evenly to obtain a mixed solution; stir the obtained mixed solution at room temperature to 95°C for 0-40 minutes, then add a solvent, and crystallize at 120-200°C for 1 ~8h, cooled to room temperature, suction filtered, and the filtered solid was dispersed in a solvent to obtain the liquid catalyst for catalyzing ozonolysis at room temperature;

所述金属盐为可溶性金属盐,选自锰盐,除此之外还可以包括铈盐、铁盐、铜盐、镍盐中的一种或两种以上任意比例的混合物;所述金属盐的形式优选为硝酸盐、硫酸盐、氯化物中的一种或多种;Described metal salt is soluble metal salt, is selected from manganese salt, can also comprise one or the mixture of two or more arbitrary proportions in cerium salt, iron salt, copper salt, nickel salt; The form is preferably one or more of nitrate, sulfate, chloride;

用于溶解金属盐的水的体积用量以金属盐的质量计为0.1~3mL/g;The volumetric amount of water used to dissolve the metal salt is 0.1-3 mL/g based on the mass of the metal salt;

所述络合剂选自EDTA、草酸、柠檬酸、抗坏血酸中的一种或两种以上任意比例的混合物;所述络合剂摩尔量与金属元素总摩尔量之比为0.1~1:1;The complexing agent is selected from one of EDTA, oxalic acid, citric acid, and ascorbic acid, or a mixture of two or more in any proportion; the ratio of the molar weight of the complexing agent to the total molar weight of metal elements is 0.1 to 1:1;

所述表面活性剂为有机表面活性剂或无机表面活性剂,优选无机表面活性剂,例如可选自六偏磷酸钠、焦磷酸钠、三聚磷酸钠中的一种或两种以上任意比例的混合物;所述表面活性剂加入质量为金属元素总质量的0.1%~2%;Described surfactant is organic surfactant or inorganic surfactant, preferably inorganic surfactant, for example can be selected from one or more arbitrary proportions in sodium hexametaphosphate, sodium pyrophosphate, sodium tripolyphosphate Mixture; the added mass of the surfactant is 0.1% to 2% of the total mass of metal elements;

混合溶液中所加入的溶剂为水和醇体积比0~1:1的混合液,体积用量以金属盐的质量计为5~10mL/g,其中所述醇为无水乙醇或乙二醇;The solvent added to the mixed solution is a mixed solution of water and alcohol at a volume ratio of 0 to 1:1, and the volume dosage is 5 to 10 mL/g based on the mass of the metal salt, wherein the alcohol is absolute ethanol or ethylene glycol;

用于分散滤出固体的溶剂为水、乙醇、丙醇的一种或两种以上任意比例的混合溶剂,其体积用量以所得固体的质量计为20~1000mL/g;The solvent used to disperse the filtered solid is water, ethanol, propanol or a mixed solvent of two or more in any proportion, and the volumetric dosage is 20-1000mL/g based on the mass of the obtained solid;

所述室温指20~30℃。The room temperature refers to 20-30°C.

本发明制得的液体催化剂(活性喷洒液)可应用于环境臭氧治理。具体应用的方法例如:将常温臭氧分解液体催化剂雾化喷洒负载于环境中任何物体表面,干燥后形成催化膜,即可对环境中的臭氧进行催化分解。The liquid catalyst (active spray liquid) prepared by the invention can be applied to environmental ozone treatment. Specific application methods, such as: atomize and spray the normal temperature ozonolysis liquid catalyst on the surface of any object in the environment, and form a catalytic film after drying, which can catalyze the decomposition of ozone in the environment.

与现有技术相比,本发明的有益效果在于:Compared with prior art, the beneficial effect of the present invention is:

1、本发明工艺简单,成本低廉,适用范围广。1. The present invention has simple process, low cost and wide application range.

2、本发明在120~200℃的较低温度下形成活性结构,可以有效防止高比表面积及丰富的氧空位因焙烧而破坏,从而获得高性能的臭氧常温分解催化剂。2. The present invention forms an active structure at a relatively low temperature of 120-200°C, which can effectively prevent high specific surface area and abundant oxygen vacancies from being destroyed by roasting, thereby obtaining a high-performance ozone decomposition catalyst at room temperature.

3、现有的臭氧常温分解催化剂制备方法普遍都通过焙烧形成最终的成型催化剂,这些常规结构的催化剂无法与高度分散的环境臭氧充分接触,很大程度上限制了催化臭氧分解的效果;而本发明制备出的是活性喷洒液,无需焙烧,理论上可以灵活地在任意形状、材质的物体表面进行雾化喷洒负载,干燥后即可赋予这些物体催化分解臭氧的能力,充分利用空间,尽可能使臭氧与催化材料充分接触,进而高效分解环境臭氧,达到治理臭氧污染的目的。3. The existing preparation methods of ozone decomposition catalysts at room temperature generally form the final shaped catalysts by roasting. These catalysts with conventional structures cannot fully contact with highly dispersed ambient ozone, which largely limits the catalytic effect of ozone decomposition; and this The invention prepares the active spray liquid without roasting. In theory, it can be flexibly atomized and sprayed on the surface of objects of any shape and material. After drying, these objects can be endowed with the ability to catalyze and decompose ozone, making full use of space. Make the ozone fully contact with the catalytic material, and then decompose the ambient ozone efficiently, so as to achieve the purpose of controlling ozone pollution.

附图说明Description of drawings

图1是实施例1制得的氧化锰常温臭氧分解液体催化剂实物图及其中活性纳米粒子的氮气吸脱附曲线图和SBETFig. 1 is the physical map of the manganese oxide room temperature ozonolysis liquid catalyst prepared in Example 1 and the nitrogen adsorption-desorption curve and S BET of the active nanoparticles therein.

图2是实施例6的活性测试图。Fig. 2 is the activity test figure of embodiment 6.

图3是实施例7~12测试装置图。Fig. 3 is a diagram of the testing device of Examples 7-12.

图4是实施例7过滤棉常温催化分解臭氧功能化。Fig. 4 is the catalytic decomposition of ozone functionalization of filter cotton at room temperature in Example 7.

图5是实施例7活性测试图。Fig. 5 is the activity test figure of embodiment 7.

图6是实施例8防晒网常温催化分解臭氧功能化。Fig. 6 is the catalytic decomposition of ozone functionalization of the sunscreen net at room temperature in Example 8.

图7是实施例8活性测试图。Fig. 7 is the activity test figure of embodiment 8.

图8是实施例9布料常温催化分解臭氧功能化。Fig. 8 is the catalytic decomposition of ozone functionalization of the fabric of Example 9 at room temperature.

图9是实施例9活性测试图。Fig. 9 is the activity test figure of embodiment 9.

图10是实施例10砖头常温催化分解臭氧功能化。Fig. 10 is the catalytic decomposition of ozone functionalization of bricks at room temperature in Example 10.

图11是实施例10活性测试图。Fig. 11 is the activity test figure of embodiment 10.

图12是实施例11石块常温催化分解臭氧功能化。Fig. 12 is the function of catalytic decomposition of ozone at room temperature of stones in Example 11.

图13是实施例11活性测试图。Fig. 13 is the activity test diagram of embodiment 11.

图14是实施例12树叶常温催化分解臭氧功能化。Fig. 14 is the catalytic decomposition of ozone functionalization of leaves in Example 12 at room temperature.

图15是实施例12活性测试图。Fig. 15 is the activity test figure of embodiment 12.

具体实施方式Detailed ways

下面通过具体实施例对本发明进行进一步描述,但本发明的保护范围并不仅限于此。The present invention will be further described below through specific examples, but the protection scope of the present invention is not limited thereto.

实施例1Example 1

将7.55g硫酸锰与1.46g EDTA、2.75×10-3g焦磷酸钠加22.7mL水配成溶液,置于70℃水浴搅拌20min,冷却后加入37.8mL水和无水乙醇混合液(体积比1:1)并转移至晶化釜,置于180℃烘箱中晶化3h,冷却至室温后进行抽滤,得到的固体加入55mL乙醇进行分散,即得到浓度为5×10-2g/mL的氧化锰常温臭氧分解液体催化剂。Make a solution of 7.55g manganese sulfate, 1.46g EDTA, 2.75×10 -3 g sodium pyrophosphate and 22.7mL water, put it in a 70°C water bath and stir for 20min, after cooling, add 37.8mL water and absolute ethanol mixture (volume ratio 1:1) and transferred to a crystallization kettle, placed in an oven at 180°C for crystallization for 3 hours, cooled to room temperature, and suction filtered. The obtained solid was dispersed by adding 55mL of ethanol to obtain a concentration of 5×10 -2 g/mL Manganese oxide room temperature ozonolysis liquid catalyst.

实施例2Example 2

将6.30g氯化锰、10.10g硝酸铁与6.75g草酸、8.29×10-2g三聚磷酸钠加49.2mL水配成溶液,置于90℃水浴搅拌30min,冷却后加入164mL水和乙二醇混合液(体积比1:1)并转移至晶化釜,置于120℃烘箱中晶化8h,冷却至室温后进行抽滤,得到的固体加入4140mL水进行分散,即得到浓度为1×10-3g/mL的锰铁二元复合氧化物常温臭氧分解液体催化剂。Mix 6.30g of manganese chloride, 10.10g of ferric nitrate, 6.75g of oxalic acid, 8.29×10 -2 g of sodium tripolyphosphate and 49.2mL of water to form a solution, place it in a water bath at 90°C and stir for 30min, after cooling, add 164mL of water and ethylene glycol Alcohol mixed solution (volume ratio 1:1) was transferred to a crystallization kettle, placed in a 120°C oven for crystallization for 8 hours, cooled to room temperature and filtered with suction, and the obtained solid was dispersed by adding 4140mL of water to obtain a concentration of 1× 10 -3 g/mL ferromanganese binary composite oxide liquid catalyst for ozonolysis at room temperature.

实施例3Example 3

将14.32g硝酸锰、8.08g硝酸铁、1.09g硝酸铈与12.0g柠檬酸、7.32×10-2g六偏磷酸钠加2.3mL水配成溶液,加入164.4mL无水乙醇并转移至晶化釜,置于140℃烘箱中晶化4h,冷却至室温后进行抽滤,得到的固体加入180mL丙醇进行分散,即得到浓度为2×10-2g/mL的锰铁铈三元复合氧化物常温臭氧分解液体催化剂。14.32g of manganese nitrate, 8.08g of ferric nitrate, 1.09g of cerium nitrate, 12.0g of citric acid, 7.32×10 -2 g of sodium hexametaphosphate and 2.3mL of water were made into a solution, and 164.4mL of absolute ethanol was added and transferred to crystallization kettle, placed in an oven at 140°C for crystallization for 4 hours, cooled to room temperature, and suction filtered. The obtained solid was dispersed by adding 180 mL of propanol to obtain a ternary composite oxidation of manganese, iron and cerium with a concentration of 2×10 -2 g/mL. A liquid catalyst for room temperature ozonolysis.

实施例4Example 4

将4.53g硫酸锰、1.62g氯化铁、0.40g硫酸铈、1.34g氯化铜与4.90g柠檬酸、2.98×10-3g三聚磷酸钠加20.0mL水配成溶液,置于60℃水浴搅拌40min,冷却后加入63.2mL无水乙醇并转移至晶化釜,置于160℃烘箱中晶化6h,冷却至室温后进行抽滤,得到的固体加入300mL水和乙醇的混合液(体积比1:1)进行分散,即得到浓度为1×10-2g/mL的锰铁铈铜四元复合氧化物常温臭氧分解液体催化剂。Make a solution of 4.53g manganese sulfate, 1.62g ferric chloride, 0.40g cerium sulfate, 1.34g copper chloride, 4.90g citric acid, 2.98×10 -3 g sodium tripolyphosphate and 20.0mL water, and place at 60°C Stir in a water bath for 40 min, add 63.2 mL of absolute ethanol after cooling and transfer to a crystallization kettle, place in a 160°C oven for crystallization for 6 h, cool to room temperature and perform suction filtration, add 300 mL of a mixed solution of water and ethanol to the obtained solid (volume ratio of 1:1) to obtain a liquid catalyst for ozone decomposition at room temperature of manganese-iron-cerium-copper quaternary composite oxide with a concentration of 1×10 -2 g/mL.

实施例5Example 5

将5.03g氯化锰、8.00g硫酸铁、0.88g氯化铈、1.60g硫酸铜、3.65g硝酸镍与21.63gEDTA、5.47×10-2g焦磷酸钠加48.0mL水配成溶液,置于室温下搅拌40min,加入115.0mL水和无水乙醇混合液(体积比0.5:1)并转移至晶化釜,置于200℃烘箱中晶化1h,冷却至室温后进行抽滤,得到的固体加入1000mL水、乙醇和丙醇的混合溶液(体积比14:5:1)进行分散,即得到浓度为5.5×10-3g/mL的锰铁铈铜镍五元复合氧化物常温臭氧分解液体催化剂。5.03g of manganese chloride, 8.00g of ferric sulfate, 0.88g of cerium chloride, 1.60g of copper sulfate, 3.65g of nickel nitrate, 21.63g of EDTA, 5.47×10 -2 g of sodium pyrophosphate and 48.0mL of water were prepared into a solution, placed in Stir at room temperature for 40 minutes, add 115.0 mL of water and ethanol mixture (volume ratio 0.5:1) and transfer to a crystallization kettle, place in a 200°C oven for crystallization for 1 hour, and suction filter after cooling to room temperature to obtain a solid Add 1000mL of mixed solution of water, ethanol and propanol (volume ratio 14:5:1) to disperse, and then obtain a five-component manganese-iron-cerium-copper-nickel composite oxide with a concentration of 5.5×10 -3 g/mL at room temperature and ozonolysis liquid catalyst.

实施例6Example 6

将实施例1制备的氧化锰常温臭氧分解液体催化剂喷洒在堇青石蜂窝陶瓷基体上,干燥后,得到负载量为2%的Mn/堇青石整体式催化剂。The manganese oxide room temperature ozonolysis liquid catalyst prepared in Example 1 was sprayed on the cordierite honeycomb ceramic substrate, and after drying, a Mn/cordierite monolithic catalyst with a loading capacity of 2% was obtained.

催化分解臭氧性能测试在固定床反应器中进行。将制得的Mn/堇青石整体催化剂(M/CH)放进U型反应管中,并置于25℃水浴。反应管中连续通入具有一定湿度(0-20h:RH=60%,20-30h:RH=40%,30-40h:RH=90%,40-45h:RH=0%)、浓度为45mg·m-3的臭氧模拟气(平衡气为空气),空速为3000h-1。尾气经红外检测,根据标准曲线转化成相应浓度,计算臭氧分解率,并以某商业臭氧分解催化剂(COC;经XRF分析,主要组成为:w(C)95.06%,w(Mn)1.39%,w(Fe)0.820%,w(Si)0.782%,w(Na)0.394%,w(Al)0.368%,w(Mg)0.214%,w(S)0.134%)作为对比,结果见图2。The catalytic ozone decomposition performance test was carried out in a fixed bed reactor. The prepared Mn/cordierite monolithic catalyst (M/CH) was put into a U-shaped reaction tube and placed in a 25°C water bath. A certain humidity (0-20h: RH=60%, 20-30h: RH=40%, 30-40h: RH=90%, 40-45h: RH=0%) is continuously introduced into the reaction tube, and the concentration is 45mg ·m -3 ozone simulation gas (balance gas is air), the space velocity is 3000h -1 . The tail gas is detected by infrared, converted into corresponding concentration according to the standard curve, and the ozone decomposition rate is calculated, and a commercial ozone decomposition catalyst (COC; XRF analysis, the main composition is: w (C) 95.06%, w (Mn) 1.39%, w (Fe) 0.820%, w (Si) 0.782%, w (Na) 0.394%, w (Al) 0.368%, w (Mg) 0.214%, w (S) 0.134%) as a comparison, the results are shown in Figure 2.

实施例7Example 7

将实施例2制备的锰铁二元复合常温臭氧分解液体催化剂喷洒在过滤棉上(如图4所示),干燥后即获得具备常温催化分解臭氧能力的过滤棉;将其置于图3所示的装置进行催化分解臭氧测试,结果如图5所示。The ferromanganese binary composite normal temperature ozonolysis liquid catalyst prepared in Example 2 is sprayed on the filter cotton (as shown in Figure 4), and after drying, the filter cotton with the ability to catalytically decompose ozone at normal temperature is obtained; it is placed as shown in Figure 3 The device shown is used for catalytic decomposition of ozone test, and the results are shown in Figure 5.

实施例8Example 8

将实施例3制备的锰铁铈三元复合常温臭氧分解液体催化剂喷洒在防晒网上(如图6所示),干燥后即获得具备常温催化分解臭氧能力的防晒网;将其置于图3所示的装置进行催化分解臭氧测试,结果如图7所示。Spray the manganese-iron-cerium ternary composite normal temperature ozonolysis liquid catalyst prepared in Example 3 on the sunscreen net (as shown in Figure 6), and obtain the sunscreen net with the ability to catalytically decompose ozone at normal temperature after drying; The device shown was used for the catalytic decomposition of ozone test, and the results are shown in Figure 7.

实施例9Example 9

将实施例4制备的锰铁铈铜四元复合常温臭氧分解液体催化剂喷洒在布料上(如图8所示),干燥后即获得具备常温催化分解臭氧能力的布料;将其置于图3所示的装置进行催化分解臭氧测试,结果如图9所示。Spray the manganese-iron-cerium-copper quaternary compound room temperature ozonolysis liquid catalyst prepared in Example 4 on the cloth (as shown in Figure 8), and obtain the cloth with room temperature catalytic decomposition of ozone after drying; place it in the place shown in Figure 3 The device shown is used for catalytic decomposition of ozone test, and the results are shown in Figure 9.

实施例10Example 10

将实施例5制备的锰铁铈铜镍五元复合常温臭氧分解液体催化剂喷洒在砖头上(如图10所示),干燥后即获得具备常温催化分解臭氧能力的砖头;将其置于图3所示的装置进行催化分解臭氧测试,结果如图11所示。Spray the manganese-iron-cerium-copper-nickel five-component composite room temperature ozonolysis liquid catalyst prepared in Example 5 on the brick (as shown in Figure 10), and obtain the brick with room temperature catalytic decomposition of ozone after drying; place it in Figure 3 The shown device was tested for catalytic decomposition of ozone, and the results are shown in FIG. 11 .

实施例11Example 11

将实施例1制备的氧化锰常温臭氧分解液体催化剂喷洒在石块上(如图12所示),干燥后即获得具备常温催化分解臭氧能力的石块;将其置于图3所示的装置进行催化分解臭氧测试,结果如图13所示。The manganese oxide room temperature ozonolysis liquid catalyst prepared in Example 1 is sprayed on the stone (as shown in Figure 12), and after drying, the stone with the ability to catalytically decompose ozone at room temperature is obtained; it is placed in the device shown in Figure 3 Carry out catalytic decomposition ozone test, the result is shown in Figure 13.

实施例12Example 12

将实施例2制备的锰铁二元复合常温臭氧分解液体催化剂喷洒在树叶上(如图14所示),干燥后即获得具备常温催化分解臭氧能力的树叶;将其置于图3所示的装置进行催化分解臭氧测试,结果如图15所示。The ferromanganese binary composite room temperature ozonolysis liquid catalyst prepared by embodiment 2 is sprayed on the leaves (as shown in Figure 14), and after drying, the leaves with the ability to catalytically decompose ozone at room temperature are obtained; The device was tested for catalytic decomposition of ozone, and the results are shown in Figure 15.

实施例13Example 13

制得的常温臭氧分解液体催化剂可雾化喷洒于环境中任意物体(路面、电线杆、墙体、布、纸等)表面,干燥后形成催化膜,即可用于催化分解环境臭氧。The prepared room temperature ozone decomposition liquid catalyst can be atomized and sprayed on the surface of any object (road, utility pole, wall, cloth, paper, etc.) in the environment, and after drying, a catalytic film can be formed, which can be used to catalyze and decompose ambient ozone.

Claims (9)

1.一种常温催化臭氧分解的液体催化剂,其特征在于,按如下方法制备得到:1. a liquid catalyst for catalytic ozonolysis at normal temperature, is characterized in that, is prepared as follows: 将金属盐溶于水,加入络合剂和表面活性剂搅拌均匀,得到混合溶液;将所得混合溶液于室温~95℃下搅拌0~40min,之后加入溶剂,在120~200℃下晶化1~8h,冷却至室温,抽滤,滤出固体分散在溶剂中,即得所述常温催化臭氧分解的液体催化剂;Dissolve the metal salt in water, add a complexing agent and a surfactant and stir evenly to obtain a mixed solution; stir the obtained mixed solution at room temperature to 95°C for 0-40 minutes, then add a solvent, and crystallize at 120-200°C for 1 ~8h, cooled to room temperature, suction filtered, and the filtered solid was dispersed in a solvent to obtain the liquid catalyst for catalyzing ozonolysis at room temperature; 所述金属盐为可溶性金属锰盐;The metal salt is a soluble metal manganese salt; 所述络合剂选自EDTA、草酸、柠檬酸、抗坏血酸中的一种或两种以上任意比例的混合物;The complexing agent is selected from one of EDTA, oxalic acid, citric acid, ascorbic acid or a mixture of two or more in any proportion; 所述表面活性剂选自六偏磷酸钠、焦磷酸钠、三聚磷酸钠中的一种或两种以上任意比例的混合物;The surfactant is selected from one of sodium hexametaphosphate, sodium pyrophosphate, sodium tripolyphosphate or a mixture of two or more in any proportion; 混合溶液中所加入的溶剂为水和醇体积比0~1:1的混合液,其中所述醇为无水乙醇或乙二醇。The solvent added to the mixed solution is a mixed solution of water and alcohol at a volume ratio of 0-1:1, wherein the alcohol is absolute ethanol or ethylene glycol. 2.如权利要求1所述常温催化臭氧分解的液体催化剂,其特征在于,所述金属盐为可溶性金属锰盐与其他可溶性金属盐的混合物,其他可溶性金属盐选自铈盐、铁盐、铜盐、镍盐中的一种或两种以上任意比例的混合物。2. the liquid catalyst of normal temperature catalytic ozonolysis as claimed in claim 1, it is characterized in that, described metal salt is the mixture of soluble metal manganese salt and other soluble metal salts, and other soluble metal salts are selected from cerium salt, iron salt, copper Salt, nickel salt, or a mixture of two or more in any proportion. 3.如权利要求1或2所述常温催化臭氧分解的液体催化剂,其特征在于,用于溶解金属盐的水的体积用量以金属盐的质量计为0.1~3mL/g。3. The liquid catalyst for catalyzing ozone decomposition at room temperature as claimed in claim 1 or 2, wherein the volumetric amount of water used to dissolve the metal salt is 0.1 to 3 mL/g based on the mass of the metal salt. 4.如权利要求1或2所述常温催化臭氧分解的液体催化剂,其特征在于,所述络合剂摩尔量与金属元素总摩尔量之比为0.1~1:1。4. The liquid catalyst for catalytic ozonolysis at room temperature according to claim 1 or 2, characterized in that the ratio of the molar weight of the complexing agent to the total molar weight of metal elements is 0.1-1:1. 5.如权利要求1或2所述常温催化臭氧分解的液体催化剂,其特征在于,所述表面活性剂加入质量为金属元素总质量的0.1%~2%。5. The liquid catalyst for catalyzing ozone decomposition at room temperature as claimed in claim 1 or 2, characterized in that the added mass of the surfactant is 0.1% to 2% of the total mass of metal elements. 6.如权利要求1或2所述常温催化臭氧分解的液体催化剂,其特征在于,混合溶液中所加入的溶剂的体积用量以金属盐的质量计为5~10mL/g。6. The liquid catalyst for catalyzing ozonolysis at room temperature as claimed in claim 1 or 2, wherein the volumetric amount of the solvent added in the mixed solution is 5-10 mL/g based on the mass of the metal salt. 7.如权利要求1或2所述常温催化臭氧分解的液体催化剂,其特征在于,用于分散滤出固体的溶剂为水、乙醇、丙醇的一种或两种以上任意比例的混合溶剂,其体积用量以所得固体的质量计为20~1000mL/g。7. as claimed in claim 1 or 2, the liquid catalyst of catalytic ozonolysis at normal temperature, is characterized in that, the solvent that is used to disperse and leach solid is water, ethanol, propanol one or two or more mixed solvents of any ratio, The volumetric dosage is 20-1000mL/g based on the mass of the obtained solid. 8.如权利要求1或2所述常温催化臭氧分解的液体催化剂在环境臭氧治理中的应用。8. the application of the liquid catalyst of catalytic ozonolysis at normal temperature as claimed in claim 1 or 2 in environmental ozone treatment. 9.如权利要求8所述的应用,其特征在于,所述应用的方法为:将常温催化臭氧分解的液体催化剂雾化喷洒负载于环境中任何物体表面,干燥后形成催化膜,即可对环境中的臭氧进行催化分解。9. The application as claimed in claim 8, characterized in that, the method of application is: atomize and spray the liquid catalyst that catalyzes ozonolysis at room temperature on the surface of any object in the environment, and form a catalytic film after drying, which can Ozone in the environment undergoes catalytic decomposition.
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